Method for preparing nap molecular sieve and nap molecular sieve with white mud as raw material

A technology of molecular sieve and lime mud, applied in the field of molecular sieve, can solve the problems of declining market competitiveness and high cost, and achieve the effect of strong market competitiveness, low production cost and high economic benefits

Active Publication Date: 2019-08-20
CHINA SHENHUA ENERGY CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, P-type molecular sieves are mainly produced by the full chemical reagent method. The raw materials are sodium metaaluminate, sodium hydroxide, and industrial grade water glass as the main raw materials. The high cost greatly reduces their market competitiveness.

Method used

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  • Method for preparing nap molecular sieve and nap molecular sieve with white mud as raw material
  • Method for preparing nap molecular sieve and nap molecular sieve with white mud as raw material
  • Method for preparing nap molecular sieve and nap molecular sieve with white mud as raw material

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043](1) Preparation of structure directing agent

[0044] First, mix sodium metaaluminate with deionized water and stir to dissolve it completely, then add sodium silicate solution to it under stirring conditions to make the Na in the system 2 O, Al 2 o 3 , SiO 2 and H 2 The molar ratio of O is 1:0.06:0.9:18, stirring at a constant temperature of 40°C for 18 hours to obtain a structure-directing agent, which is then sealed and kept at a constant temperature for later use;

[0045] (2) Preparation of silicon source and aluminum source

[0046] Add 240ml of 4mol / L sodium hydroxide solution to 40g white mud for leaching (the mass ratio of sodium hydroxide and white mud is 1:0.96), to leach soluble silicon and aluminum, then filter, and collect the filtrate for subsequent use ; Among them, the alkali leaching temperature is 70°C, and the alkali leaching time is 4h; SiO 2 、Al 2 o 3 The extraction rates were 56.99% and 23.06% respectively;

[0047] (3) Preparation of sili...

Embodiment 2

[0055] (1) Preparation of structure directing agent

[0056] First, mix sodium metaaluminate with deionized water and stir to dissolve it completely, then add sodium silicate solution to it under stirring conditions to make the Na in the system 2 O, Al 2 o 3 , SiO 2 and H 2 The molar ratio of O is 1:0.05:0.7:20, stirring at a constant temperature of 25°C for 24 hours to obtain a structure-directing agent, which is then sealed and kept at a constant temperature for later use;

[0057] (2) Preparation of silicon source and aluminum source

[0058] Add 240ml of 3.5mol / L sodium hydroxide solution to 40g white mud and leach it (the mass ratio of sodium hydroxide and white mud is 1:0.84), to leach soluble silicon and aluminum, then filter and collect the filtrate Standby; among them, the alkali leaching temperature is 60°C, and the alkali leaching time is 4.5h; SiO 2 、Al 2 o 3 The extraction rates were 56.56% and 20.25% respectively;

[0059] (3) Preparation of silica-alumi...

Embodiment 3

[0067] (1) Preparation of structure directing agent

[0068] First, mix sodium metaaluminate with deionized water and stir to dissolve it completely, then add sodium silicate solution to it under stirring conditions to make the Na in the system 2 O, Al 2 o 3 , SiO 2 and H 2 The molar ratio of O is 1:0.07:1.1:16, stirring at a constant temperature of 50°C for 12 hours to obtain a structure-directing agent, which is then sealed and kept at a constant temperature for later use;

[0069] (2) Preparation of silicon source and aluminum source

[0070] Add 240ml of 5mol / L sodium hydroxide solution to 40g white mud for leaching (the mass ratio of sodium hydroxide and white mud is 1:1.2), to leach soluble silicon and aluminum, then filter, and collect the filtrate for subsequent use ; Among them, the alkali leaching temperature is 80 ℃, and the alkali leaching time is 3.5h; SiO 2 、Al 2 o 3 The extraction rates were 55.81% and 23.59% respectively;

[0071] (3) Preparation of si...

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PUM

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Abstract

The invention provides a method for preparing a NaP molecular sieve from white mud as a raw material and the NaP molecular sieve. The method comprises the steps of (1) preparing a structure-directing agent; (2) preparing a silicon source and an aluminum source, namely extracting the white mud by using a sodium hydroxide solution, filtering and collecting filtrate for later use; (3) preparing silica-alumina gel, namely adding sodium metaaluminate and deionized water to the filtrate until the molar ratio of SiO2 to Al2O3 in the system is (2-3):1 and the molar ratio of Al to H2O is 1:(360-495), adjusting the pH value of the system to be 10-11, adding the structure-directing agent, stirring evenly and ageing to obtain the silica-alumina gel; (4) crystallizing the silica-alumina gel; and (5) carrying out post-treatment, namely filtering a crystalized product and then washing and drying the filtered product to obtain the NaP molecular sieve. According to the method, the NaP molecular sieve can be prepared by fully utilizing effective silicon and aluminum in the white mud, the waste utilization of the white mud is achieved, the preparation cost of the NaP molecular sieve is reduced and the prepared NaP molecular sieve is good in performance, large in ion exchange capacity and high in economic benefit.

Description

technical field [0001] The invention belongs to the field of molecular sieves, in particular to a method for preparing NaP molecular sieves from white mud and the NaP molecular sieves. Background technique [0002] Shenhua Group has successfully developed the world's first "one-step acid-dissolution method" new process for producing alumina from fly ash based on the characteristics of high-aluminum fly ash produced after coal combustion in the Zhungeer area. Please refer to the patent document CN102145905A. According to the process calculation, every 2.5 tons of fly ash produces 1 ton of metallurgical grade alumina and 1.5 tons of high silicon tailings (white mud). The composition of the white mud is shown in Table 1, where Los represents the loss on ignition of the white mud, and each component is represented by the oxide form of each element. [0003] The composition of table 1 white mud and the content of each composition [0004] [0005] It can be seen from Table 1...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B25/08C01B37/00C01B39/00
Inventor 李超王永旺王丽萍陈东贾敏高桂梅杜艳霞王强
Owner CHINA SHENHUA ENERGY CO LTD
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